Dissertations / Theses on the topic 'Fuel'
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Preece, John Christopher. "Oxygenated hydrocarbon fuels for solid oxide fuel cells." Thesis, University of Birmingham, 2006. http://etheses.bham.ac.uk//id/eprint/117/.
Full textHung, Tak Cheong. "Fuel reforming for fuel cell application /." View abstract or full-text, 2006. http://library.ust.hk/cgi/db/thesis.pl?CENG%202006%20HUNG.
Full textROMANATO, LUIZ S. "Armazenagem de combustivel nuclear queimado." reponame:Repositório Institucional do IPEN, 2005. http://repositorio.ipen.br:8080/xmlui/handle/123456789/11204.
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Dissertacao (Mestrado)
IPEN/D
Instituto de Pesquisas Energeticas e Nucleares, IPEN/CNEN-SP
Zhang, Mingming. "Properties of bio-oil based fuel mixtures: biochar/bio-oil slurry fuels and glycerol/bio-oil fuel blends." Thesis, Curtin University, 2015. http://hdl.handle.net/20.500.11937/1825.
Full textClarke, Adrian James. "The conceptual design of novel future UAV's incorporating advanced technology research components." Thesis, Cranfield University, 2011. http://dspace.lib.cranfield.ac.uk/handle/1826/7163.
Full textLeung, Chin Pui Perry. "Exhaust gas fuel reforming to achieve fuel saving." Thesis, University of Birmingham, 2013. http://etheses.bham.ac.uk//id/eprint/4330/.
Full textDeGolyer, Jessica Suzanne. "Fuel Life-Cycle Analysis of Hydrogen vs. Conventional Transportation Fuels." NCSU, 2008. http://www.lib.ncsu.edu/theses/available/etd-08192008-124223/.
Full textLee, Won Yong Ph D. Massachusetts Institute of Technology. "Mathematical modeling of solid oxide fuel cells using hydrocarbon fuels." Thesis, Massachusetts Institute of Technology, 2012. http://hdl.handle.net/1721.1/74906.
Full textCataloged from PDF version of thesis.
Includes bibliographical references.
Solid oxide fuel cells (SOFCs) are high efficiency conversion devices that use hydrogen or light hydrocarbon (HC) fuels in stationary applications to produce quiet and clean power. While successful, HC-fueled SOFCs face several challenges, the most significant being performance degradation due to carbon deposition and the need of external reforming when using heavier HC. Modeling these devices faces these as well as other complexities such as the presence of multiple electrochemistry pathways including those of H2 and CO. The goals of this thesis are to: (1) improve the thermodynamic analysis of carbon deposition, (2) develop a multistep CO electrochemistry mechanism, and (3) apply the CO along with the H2 electrochemistry mechanisms to predict the cell performance when using syngas. Two carbon deposition mechanisms have been identified: homogeneously formed soot and catalytically grown carbon fiber. All previous thermodynamic analyses have used graphite to represent the properties of the deposited carbon regardless of the formation mechanism. However, the energetic and entropic properties of these two types of carbon are different from those of graphite. A new thermodynamic analysis is proposed that: (1) uses experimentally measured data for carbon fiber if the anode includes Ni catalyst; and (2) uses soot precursors such as CH3 and C2H2 to predict soot formation. The new approach improves the prediction of the onset of carbon deposition where previous analyses failed. A new multi-step CO electrochemistry model is proposed in which CO is directly involved in the charge-transfer steps. The model structure, with a single set of kinetic parameters at each temperature, succeeds in reproducing the characteristics of the EIS data of patterned anodes including the inductive loop at high activation overpotential. The model successfully predicts the steady-state Tafel plots, and explains the positive dependence of the exchange current density on Pco2 - Finally, a membrane-electrode-assembly (MEA) model is developed incorporating multispecies transport through the porous structure, detailed elementary heterogeneous reactions on the Ni surface, and for the first time, detailed electrochemistry models for H2 and CO. The model successfully reproduces the performance of SOFCs using pure H2 or CO. The MEA model can isolate/distinguish between the roles/contributions of the reforming chemistry and CO electrochemistry in SOFCs using syngas. Adding reforming thermochemistry improves the agreement with experiments at lower current densities, and raises the limiting current density by providing more H2 via the water-gas shift reaction. Adding CO electrochemistry improves the prediction at high current densities by the additional current generated by the CO electrochemical oxidation. The current from CO becomes comparable to that from H2 as the CO content at the TPB increases.
by Won Yong Lee.
Ph.D.
Lively, Treise. "Ethanol fuel cell electrocatalysis : novel catalyst preparation, characterization and performance towards ethanol electrooxidation." Thesis, Queen's University Belfast, 2013. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.602560.
Full textMatter, Paul H. "Electrocatalytic and fuel processing studies for portable fuel cells." Columbus, Ohio : Ohio State University, 2006. http://rave.ohiolink.edu/etdc/view?acc%5Fnum=osu1149037376.
Full textSalih, Fawzi Mohamed. "Automotive fuel economy measures and fuel usage in Sudan." Thesis, University of Leeds, 1990. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.293763.
Full textAquien, Alexandre. "Fuel cycle options for optimized recycling of nuclear fuel." Thesis, Massachusetts Institute of Technology, 2006. http://hdl.handle.net/1721.1/42340.
Full textPage 200 blank.
Includes bibliographical references (p. 170-171).
The accumulation of transuranic inventories in spent nuclear fuel depends on both deployment of advanced reactors that can be loaded with recycled transuranics (TRU), and on availability of the facilities that separate and reprocess spent fuel. Three recycling strategies are explored in this study: (1) Recycling in thermal Light 'Water Reactors (LWR) using CONFU technology (COmbined Non-Fertile and UO2 fuel), (2) recycling of TRU in fast cores of Actinide Burner Reactors (ABR), and (3) recycling of TRU with UO2 in self-sustaining Gas-cooled Fast Reactors (GFR). Choosing one fuel cycle strategy over the others involves trade-offs that need to be quantified. The CONFU, ABR, and GFR strategies differ from each other in terms of TRU loading in the reactor, net TRU incineration, capacities of recycling facilities needed, technology option availability, and flexibility. The CONFU and GFR are assumed to achieve zero net TRU incineration, while the ABR is a net consumer of TRU. The TRU loading is greatest in GFR and lowest in CONFU. While both CONFU and ABR require separation (of TRU from U) and reprocessing (recycling of TRUs from fertile-free fuel), the GFR is designed to, in equilibrium, recycle TRU+U after extraction of fission products only. It is assumed that thermal recycling is available in the short-term (2015), as opposed to recycling in fast reactors (2040). Finally, thermal recycling is the most flexible as either CONFU batches or regular LWR uranium batches can be loaded; the issue of running out of TRU fuel is therefore irrelevant for this option. A fuel cycle simulation tool, CAFCA II - Code for Advanced Fuel Cycles Assessment - has been developed. The CAFCA II code tracks the mass distribution of TRU in the system and the cost of all operations.
(cont.) The code includes a specific model for recycling plants deployment; as an industrial process occurring in facilities with given capacities and investment requirements. These facilities may operate with a minimum target capacity factor during the lifetime of the plant. The deployment of these facilities is also constrained by a user-specified ability to add recycling capacity within a given time interval. Finally, the CAFCA II code includes a specific model for recycling prices as a function of plants nominal capacities, which reflects the economies of scale that go with increasing the nominal capacity of recycling plants. Our first case-study identifies the optimal choice of fuel cycle option and recycling plants capacities as a function of the deployment of advanced fuel cycle technologies over the next hundred years and under the assumption of the US demand for nuclear energy growing at a 2.4% annual rate. Key figures of merit for comparison of the strategies are the reduction of TRU interim storage requirements, the maximization of TRU incineration, the minimization of the size of the fleets of recycling plants and fast reactors, and the fuel cycle cost. We found that it is not possible to minimize simultaneously (1) the construction rate of advanced reactors and advanced spent fuel recycling facilities, and (2) the construction rate of U02 spent fuel separation facilities. The latter was found to be more constraining than the first for purposes of TRU inventories reduction. We found also that reactor technologies with zero net TRU destruction rate can achieve total depletion of TRU inventories is spent fuel interim storage at a lower fuel cycle cost and with fewer recycling facilities than reactor technologies that incinerate TRU; the lower fuel cycle cost is achieved at the expense of a lesser reduction of total TRU inventories.
(cont.) Finally, we found that, if the construction rate of advanced nuclear technologies is large enough, the later introduction date of fast recycling schemes compared to thermal recycling schemes is not discriminatory, with regards to the reduction of TRU inventories in interim storage by 2100. The potential of multi-lateral approaches to the nuclear fuel cycle has recently been widely acknowledged. Cited benefits include cost attractiveness following from economies of scale, proliferation resistance and collaborative and more efficient nuclear waste treatment strategy. CAFCA II has been developed to quantify these trade implications for the back-end of the fuel cycle Three bi-lateral scenarios of partnerships have been examined between two regions: first a scenario where the "Fuel-leasing/fuel take-back" concept is implemented, second a scenario with "Limited Collaboration" at the back-end fuel cycle, where spent fuel recycling and advanced fuel fabrication are externalized in countries that have these technologies, and third a scenario of "Full Collaboration", under which two regions fully collaborate at the fuel cycle back-end: spent fuel inventories and advanced fuel cycle facilities are co-owned and comanaged. Our second case-study concentrates on optimizing the choice of (1) fuel cycle option, (2) spent fuel recycling plant capacities, and (3) partnership scenario by analyzing the implications of these choices for the LWR-CONFU, LWR/ABR, and LWR/GFR strategies. The nuclear fuel cycle is simulated in a two-region context from 2005 to 2100 under the assumption that one region represents the US growing at a 2.4% annual rate and the other region represents Brazil, Indonesia, and Mexico growing at a 7.4% annual rate until 2080, and at 2.4% afterwards.
(cont.) We found that a US partnership with Brazil, Mexico, and Indonesia, could be advantageous to the reduction of TRU storage in both regions if the construction rate of UO2 spent fuel separation plants would be larger than one 1,000 MT/yr plant every two years after 2050. We found also that, from the point of view of the spent fuel recycling industry, use of largest recycling plants with the lowest construction cost per unit of installed capacity becomes optimal only with multi-national approaches to the fuel cycle back-end.
by Alexandre Aquien.
S.M.
Flora, Giacomo. "Fuel Structure Effects on Surrogate Alternative Jet Fuel Emission." University of Dayton / OhioLINK, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=dayton1450286398.
Full textSinuka, Yonwaba. "Performance testing of a diesel engine running on varying blends of jatropha oil, waste cooking oil and diesel fuel." Thesis, Cape Peninsula University of Technology, 2016. http://hdl.handle.net/20.500.11838/2436.
Full textThe high cost of fossil fuels and the fact that the world has arguably reached its peak oil production, has driven the need to seek alternative fuel sources. The main objective of the current study is to determine the performance of a laboratory-mounted diesel engine when fuelled with varying laboratory prepared biofuel and biodiesel and whether the advancement of the injection timing parameters will improve the engine power output and improve the smoke effect of these different fuel blends. The laboratory prepared biofuels used in this project range from 100% bio-fuel (BF100) to 50%, 30% and 10% biodiesel blends (BF50, BF30 and BF10, respectively). It should be noted that these blends are not commercially available, since they were blended in the laboratory specifically for these tests. The overall results of the study show that there is a distinct opportunity for using certain bio-fuel blends in specific applications as the power outputs are no more than one quarter less than that of base diesel. Concomitantly, the smoke opacity in all of the blends is lower than that of base diesel, which is a significant benefit in terms of their overall air emissions.
Rohaly, Matthew Joseph. "Decomposition of Aromatic Amines in a Jet Fuel Surrogate." University of Dayton / OhioLINK, 2014. http://rave.ohiolink.edu/etdc/view?acc_num=dayton1417777531.
Full textHuang, Lloyd Michael. "Analysis of multi-recycle thorium fuel cycles in comparison with once-through fuel cycles." Thesis, Georgia Institute of Technology, 2013. http://hdl.handle.net/1853/47662.
Full textMarquez, Matias G. "Silicide fuel swelling behavior and its performance in I2S-LWR." Thesis, Georgia Institute of Technology, 2015. http://hdl.handle.net/1853/53970.
Full textROMANATO, LUIZ S. "Estudo de um casco nacional e sua instalacao para armazenagem seca de combustivel nuclear queimado gerado em reatores PWR." reponame:Repositório Institucional do IPEN, 2009. http://repositorio.ipen.br:8080/xmlui/handle/123456789/9476.
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Tese (Doutoramento)
IPEN/T
Instituto de Pesquisas Energeticas e Nucleares - IPEN-CNEN/SP
Chandler, Sharon (Jess) Ann. "Comparison of Reprocessing Methods for Light Water Reactor Fuel." Thesis, Georgia Institute of Technology, 2006. http://hdl.handle.net/1853/14018.
Full textSukjit, Ekarong. "Synergistic effects of alcohol-based renewable fuels : fuel properties and emissions." Thesis, University of Birmingham, 2013. http://etheses.bham.ac.uk//id/eprint/4674/.
Full textMirzababaei, Jelvehnaz. "Solid Oxide Fuel Cells with Methane and Fe/Ti Oxide Fuels." University of Akron / OhioLINK, 2014. http://rave.ohiolink.edu/etdc/view?acc_num=akron1415461807.
Full textStutz, Michael Jun. "Hydrocarbon fuel processing of micro solid oxide fuel cell systems." Zürich : ETH, 2007. http://e-collection.ethbib.ethz.ch/show?type=diss&nr=17455.
Full textGerber, Chad A., and Jeremy A. Clark. "More fightless-fuel: reducing fuel burn through ground process improvement." Monterey, California: Naval Postgraduate School, 2013. http://hdl.handle.net/10945/34667.
Full textAligning fiscal policies with energy conservation initiatives and operational requirements is vital to achieving a positive and sustainable energy outlook for the United States Navy. The purpose of this study is to fill critical gaps in current military aviation energy conservation research. To date, such research has failed to incentivize and reward individual aviation squadrons to conserve. Commercial aviation uses collaborative decision-making (CDM) tools to minimize costs associated with aircraft delays. Embracing a lean approach to operational management, the commercial sector has refined communications between air carriers, airport operators, ground handlers, and air traffic control. This study suggests applying commercial CDM frameworks to all of Naval Aviation to increase efficiency and operational effectiveness. Specific analysis includes the impact of ground resource capacity management, airfield demand analysis (slot arrival system) and demand management cost analysis on F/A-18 Hornet squadrons.
Nabity, James Allen. "Metallized fuel particle size study in a solid fuel ramjet." Thesis, Monterey, California. Naval Postgraduate School, 1989. http://hdl.handle.net/10945/26063.
Full textReese, Drew A. (Drew Amelia). "Dependence of transuranic content in spent fuel on fuel burnup." Thesis, Massachusetts Institute of Technology, 2007. http://hdl.handle.net/1721.1/41692.
Full textIncludes bibliographical references (p. 33).
As the increasing demand for nuclear energy results in larger spent fuel volume, implementation of longer fuel cycles incorporating higher burnup are becoming common. Understanding the effect of higher burnup on the spent fuel composition and radioactive properties is essential to ensure that spent fuel receives proper cooling in storage before it is sent to a disposal site or proper treatment and reprocessing if its useful content is to be extracted prior to disposal. Using CASMO-4, a standard Westinghouse 4-loop pressurized water reactor model was created and simulated with a three batch fuel cycle. U-235 enrichment was adjusted to achieve fuel burnups of 30, 50, 70 and 100 MWD per kg of initial uranium. These burnups demanded reload enrichments of 3.15%, 4.63%, 6.26% and 9.01% U-235 w/o respectively. The resultant spent fuel transuranic isotopic compositions were then provided as input into ORIGEN to study the decay behavior of the spent fuel. It was found that when burnup increased from 30 MWD/kg to 100 MWD/kg, the activity more than doubled due to the decreased Pu-241 content and the increased Np-239 presence. More importantly, the activity per MWD significantly decreased despite absolute increases in unit mass. The net result is that the half-life of high burnup fuels is greatly increased in comparison to low burnup fuels for the first decade of life. Beginning from day 14 after shutdown and until 10 years later, the 100 MWD/kg fuel has a half-life of 129 days while the 30 MWD/kg spent fuel has a half life of 5 days. Previous work has suggested that different trends dominate decay behavior from years 10 to 100 years following discharge.
by Drew A. Reese.
S.B.
Zino, John Frederick. "Analysis of subcritical experiments using fresh and spent research reactor fuel assemblies." Diss., Georgia Institute of Technology, 1999. http://hdl.handle.net/1853/17507.
Full textChen, Guoqiang. "Fuel volatility modeling." Thesis, Massachusetts Institute of Technology, 1994. http://hdl.handle.net/1721.1/12282.
Full textGutiérrez, Daniel. "Green Fuel Simulations." Thesis, Luleå tekniska universitet, Institutionen för teknikvetenskap och matematik, 2020. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-79244.
Full textPinto, Maria Jorge Pratas de Melo. "Biodiesel fuel formulation." Doctoral thesis, Universidade de Aveiro, 2012. http://hdl.handle.net/10773/9328.
Full textO consumo de energia a nível mundial aumenta a cada dia, de forma inversa aos recursos fósseis que decrescem de dia para dia. O sector dos transportes é o maior consumidor deste recurso. Face ao actual cenário urge encontrar uma solução renovável e sustentável que permita não só, diminuir a nossa dependência de combustíveis fósseis mas fundamentalmente promover a sua substituição por energias de fontes renováveis. O biodiesel apresenta-se na vanguarda das alternativas aos combustiveis derivados do petróleo, para o sector dos transportes, sendo considerado uma importante opção a curto prazo, uma vez que o seu preço pode ser competitivo com o diesel convencional, e para a sua utilização o motor de combustão não necessita de alterações. O biodiesel é uma mistura líquida, não tóxica, biodegradável de ésteres de ácidos gordos, sem teor de enxofre ou compostos aromáticos, apresenta boa lubricidade, alto número de cetano, e origina emissões gasosas mais limpas. O presente trabalho contribui para um melhor conhecimento da dependência das propriedades termofisicas do biodiesel com a sua composição. A publicação de novos dados permitirá o desenvolvimento de modelos mais fiáveis na previsão do comportamento do biodiesel. As propriedades densidade e viscosidade são o espelho da composição do biodiesel, uma vez que dependem directamente da matéria prima que lhe deu origem, mais do que do processo de produção. Neste trabalho os dados medidos de densidade e viscosidade de biodiesel foram testados com vários modelos e inclusivamente foram propostos novos modelos ajustados para esta família de compostos. Os dados medidos abrangem uma ampla gama de temperaturas e no caso da densidade também foram medidos dados a alta pressão de biodiesel e de alguns ésteres metilico puros. Neste trabalho também são apresentados dados experimentais para o equilíbrio de fases sólido-liquído de biodiesel e equlibrio de fases líquidolíquido de alguns sistemas importantes para a produção de biodiesel. Ambos os tipos de equilíbrio foram descritos por modelos desenvolvidos no nosso laboratório. Uma importância especial é dado aqui a propriedades que dependem do perfil de ácidos gordos da matéria-prima além de densidade e viscosidade; o índice de iodo e temperature limite de filtrabalidade são aqui avaliados com base nas considerações das normas. Os ácidos gordos livres são um sub-produto de refinação de óleo alimentar, que são removidos na desodoração, no processo de purificação do óleo. A catálise enzimática é aqui abordada como alternativa para a conversão destes ácidos gordos livres em biodiesel. Estudou-se a capacidade da lipase da Candida antartica (Novozym 435) para promover a esterificação de ácidos gordos livres com metanol ou etanol, utilizando metodologia de superfície de resposta com planeamento experimental. Avaliou-se a influência de diversas variáveis no rendimento da reacção.
World energy consumption rises every day and, inversely, fossil fuel resources are dwindling day by day. Transportation sector is the bigger consumer of oil. Faced with the actual scenario a renewable and sustenable alternative is needed, not just to decrease our dependence of petroleum but also to base our power in a renewable source. Biodiesel is at the forefront of the alternatives to petroleum based fuels in the transportation sector, being considered an important short-time option since its price can be competitive with conventional diesel and no motor changes are required. Biodiesel consists on a liquid blend of, non toxic, biodegradable fatty acid esters, with non sulfur and aromatic content, good lubricity, high cetane number, nontoxic character of their exhaust emissions and cleaner burning. Aiming at tuning biodiesel to optimize the fuel composition, the present work contributes for a better knowledge of de depencende of thermophysical properties of biodiesel on their compositon. New data is required to help in the development of reliable models to predict biodiesel behavior. Density and viscosity data are a mirror of biodiesel composition, as both depend on the raw material, more than the production process. New data of density and viscosity were measured and respective models were tested and compared, and new adjusted parameters proposed for this family of compounds. The measured data include a wide range of temperatures and in the case of density data were also measured at high pressure for biodiesel and some pure methyl esters. This work also reports experimental data for the solid-liquid-phase equilibria of biodiesel and, liquid-liquid equilibria of some important systems in biodiesel production. Both type of equilibria were described with models developed in our laboratory. A special importance is here given to properties that depend on fatty acid profile of raw material besides density and viscosity; the iodine value, and cold filter plugging point are here evaluated based on norm considerations. Free Fatty Acids (FFA) are a by-product in edible oil refining, that are removed in the deodorizing step on oil purification. Enzymatic catalysis is here studied as an alternative to convert this by-product into biodiesel. The ability of immobilized lipase from Candida antartica (Novozym 435) to catalize the esterification of FFA with methanol and ethanol were evaluated using response surface methodology with an experimental design. Influence of several variables were evaluated in the yield of reaction.
Lim, Keng Guan. "Microfluidic fuel cell." View abstract/electronic edition; access limited to Brown University users, 2008. http://gateway.proquest.com/openurl?url_ver=Z39.88-2004&rft_val_fmt=info:ofi/fmt:kev:mtx:dissertation&res_dat=xri:pqdiss&rft_dat=xri:pqdiss:3319104.
Full textMurray, K. D. "Biochemical fuel cells." Thesis, University of Bath, 1988. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.380401.
Full textLang, Kevin R. 1980. "Effect of fuel properties on the first cycle fuel delivery in a Port Fuel Injected Spark Ignition Engine." Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/27074.
Full textIncludes bibliographical references (p. 73-74).
Achieving robust combustion while also yielding low hydrocarbon (HC) emissions is difficult for the first cycle of cranking during the cold start of a Port Fuel Injected (PFI) Spark Ignition (SI) engine. Cold intake port wall and valve temperatures, near-atmospheric manifold pressure, and low port air velocity combine to create an adverse environment for fuel delivery - the process of injecting and vaporizing liquid fuel to create a combustible air-fuel mixture. As a result, only a small fraction of the injected fuel mass contributes to the combustible mixture; the fraction is less than 10% at cold ambient temperatures. With fast light off catalysts, the first cycle produces a significant portion of the total trip emissions. The low fuel delivery fraction results in high residual liquid fuel in both the port and cylinder; this fuel contributes significantly to the exhaust HC emissions. Since the first cycle engine control is open-loop, the Engine Control Unit (ECU) must determine how much fuel to inject under given conditions - temperature, pressure, and for a given fuel. Fuel properties play a significant role in first cycle fuel delivery, since the energy available for vaporization is a limiting factor in fuel delivery. The effect of fuel properties on fuel delivery for the first cycle was quantified at a wide range of cold start temperatures by using a skip-firing strategy to simulate the first cycle of cranking on a production PFI engine. Four fuels between 1083 and 1257 Driveability Index (DI) were tested, and the fuel delivery results have been correlated to properties of the ASTM distillation curve. The fractional distillation point that correlates to fuel delivery is a function of temperature - at colder temperatures, the results
(cont.) correlate with the more volatile end of the distillation curve. Fuel delivery results for the fuels were also simulated with a thermodynamics-based fuel delivery model based on partial equilibrium with the charge air.
by Kevin R. Lang.
S.M.
Reece, Warren Daniel. "Theory of cladding breach location and size determination using delayed neutron signals /." Diss., Georgia Institute of Technology, 1988. http://hdl.handle.net/1853/13317.
Full textPESSOA, JOAO S. "Projeto piloto do etanol - PPE. Alternativa energetica para substituicao parcial ou total do oleo combustivel em plantas de geracao termoeletrica." reponame:Repositório Institucional do IPEN, 2004. http://repositorio.ipen.br:8080/xmlui/handle/123456789/11185.
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Dissertacao (Mestrado)
IPEN/D
Instituto de Pesquisas Energeticas e Nucleares - IPEN/CNEN-SP
Sommer, Christopher Michael. "Subcritical transmutation of spent nuclear fuel." Diss., Georgia Institute of Technology, 2011. http://hdl.handle.net/1853/41205.
Full textChen, Eric L. "Testing and modelling of a fuel cell and a fuel processor." Thesis, University of Oxford, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.394009.
Full textCuseo, James M. (James Michael). "Cold start fuel management of port-fuel-injected internal combustion engines." Thesis, Massachusetts Institute of Technology, 2005. http://hdl.handle.net/1721.1/32380.
Full textIncludes bibliographical references (p. 64).
The purpose of this study is to investigate how changes in fueling strategy in the second cycle of engine operation influence the delivered charge fuel mass and engine out hydrocarbon (EOHC) emissions in that and subsequent cycles. Close attention will be paid to cycle-to-cycle interaction of the fueling strategy. It is our intent to see if residual fuel from each cycle has a predicable influence on subsequent cycle's charge mass and EOHC emissions. The fast flame ionization detector is employed to measure both in-cylinder and engine out hydrocarbon concentrations for various cold start strategies. The manufacturer's original fueling strategy is used as a starting point and is compared to a "in-cylinder fuel air ratio (Phi) [approx.] 1" case (a fueling strategy that results in an in-cylinder concentration of approximately stoichiometric for each of the first five cycles) and to a number of cases that are chosen to illustrate cycle-to-cycle mixture preparation dependence on second cycle fueling. Significant cycle-to-cycle dependence is observed with the change in second cycle. A fueling deficit in cycle two has a more pronounce effect on future cycles delivered charge mass than a fueling surplus while a fueling surplus in cycle two has a more pronounce effect on future cycles charge mass than a fueling deficit.
by James M. Cuseo.
S.M.
Saxe, Maria. "Bringing fuel cells to reality and reality to fuel cells : A systems perspective on the use of fuel cells." Doctoral thesis, KTH, Energiprocesser, 2008. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-9192.
Full textQC 20100909
Energy Systems Programme
Clean Urban Transport for Europe
GlashusEtt
Vittilapuram, Subramanian Kannan. "Modelin combustion of multicomponent fuel droplets: formulation and application to transportation fuels." Texas A&M University, 2004. http://hdl.handle.net/1969.1/3320.
Full textFarao, Javon. "Toward a full aircraft model platform for fuel slosh-structure interaction simulations." Master's thesis, University of Cape Town, 2015. http://hdl.handle.net/11427/24315.
Full textAbdullah, Hanisom binti. "High energy density fuels derived from mallee biomass: fuel properties and implications." Thesis, Curtin University, 2010. http://hdl.handle.net/20.500.11937/2259.
Full textVerma, Saket. "Experimental investigation and exergy analysis of a dual fuel engine using alternative fuels." Thesis, IITD, 2019. http://eprint.iitd.ac.in:80//handle/2074/8099.
Full textIon, Robert Aurelian. "Fuel depletion analyses at the Missouri University Research Reactor." Diss., Columbia, Mo. : University of Missouri-Columbia, 2006. http://hdl.handle.net/10355/5903.
Full textThe entire dissertation/thesis text is included in the research.pdf file; the official abstract appears in the short.pdf file (which also appears in the research.pdf); a non-technical general description, or public abstract, appears in the public.pdf file. Title from title screen of research.pdf file viewed on (March 2, 2007) Vita. Includes bibliographical references.
McHenry, John Carl Izaak. "The Challenges of Biofuels in Ohio: From the Perspective of Small-Scale Producers." Ohio : Ohio University, 2008. http://www.ohiolink.edu/etd/view.cgi?ohiou1197926303.
Full textShelby, Michael H. (Michael Howard). "PLIF investigation of the fuel distribution in gasoline direct injection fuel sprays." Thesis, Massachusetts Institute of Technology, 1997. http://hdl.handle.net/1721.1/43930.
Full textWelling, Orian (Orian Z. ). "Thin fuel film reactor testing for characterization of diesel fuel deposit formation." Thesis, Massachusetts Institute of Technology, 2009. http://hdl.handle.net/1721.1/54481.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 29-30).
The need for specialized diesel fuel injectors is growing with increased efficiency and emissions regulation. These specialized fuel injectors have nozzle diameters of 150-200[mu]m which are susceptible to clogging from deposit formation. This thesis studies the deposit formation mechanisms with a thin fuel film reactor, and examines the potential for use of the reactor as a detergent screening tool. Through experimentation with the thin fuel film reactor it was found that temperature had negligible effect on the weight of a fully dried fuel film. This suggests that testing could be conducted at high or low temperatures to decrease the cycle time or increase test resolution respectively. It was also determined that dry deposits remain soluble in hot fuel immediately following drying, but become insoluble after long hot soak periods. A simple deposit formation model was constructed based on hypothesized formation factors. Although very simplified, the model matched the experimental results well. The correlation suggest that the hypothesized formation factors are critical to the formation process. The model should be expanded to explain deposit formation more generally, and further research should be conducted to better validate the model.
by Orian Welling.
S.B.
Sheikhansari, Abdolkarim. "Evaluation of solid oxide fuel cells operating on hydrogen sulfide contaminated fuel." Thesis, University of Sheffield, 2017. http://etheses.whiterose.ac.uk/17699/.
Full textEriksson, John, and Mårten Wallengren. "Model Based Control Algorithm for a Bi-Fuel Engine with fuel adjustment." Thesis, KTH, Maskinkonstruktion (Inst.), 2013. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-141183.
Full textA little more than a hundred years ago the first mass produced car rolled of the assembly line, in the optional color black, and since then a hectic race has been going on in order to improve all parts of the car. First only as a competitive edge with bigger engines and more comfort for the passengers, but in the last decades also as a response to increased legislation's around the world in order to be able to sell to their respective market. Apart from increasing the effectiveness of both engine and catalyst in order to meet the ever increasing environmental demands, there is also the possibility of exchanging the fuel used. One prominent alternative here is Compressed Natural Gas (CNG), that can be extracted both from natural gas or biogas, dependent on what available resources are at hand. In order to accommodate this change in fuel Anstalt fur Verbrennungskraftmaschinen List (AVL) has the desire to further develop its engine control software Rap2L, inorder to also be able to run CNG engines. The purpose for this thesis is to build a separate add-on to Rap2L where all the functionality for CNG is handled, it should also be able to, with minimal effort, be transported to another engine control system, if so desired.
Bath, Andrew. "Performance Characterization of Complex Fuel Port Geometries for Hybrid Rocket Fuel Grains." DigitalCommons@USU, 2012. https://digitalcommons.usu.edu/etd/1381.
Full textTshizanga, Ngoya. "A study of biodiesel production from waste vegetable oil using eggshell ash as a heterogeneous catalyst." Thesis, Cape Peninsula University of Technology, 2015. http://hdl.handle.net/20.500.11838/2153.
Full textWhile biodiesel has the potential to resolve the energy crisis, its production is hampered by both feedstock and catalyst availability. The aim of this current study is to investigate the production of biodiesel from waste vegetable oil (WVO) as feedstock under heterogeneous catalysis, mediated by calcined eggshell ash. WVO, characterised by 9% free fatty acid (FFA) and 0.17wt% water content, was employed as feedstock in the biodiesel production via transesterification reaction. The composition of WVO was determined using Gas chromatography (GC) analysis. The eggshell was washed with distilled water to remove impurities, dried in an oven at 105°C, and then crushed into fine particle of 75μm, and finally, calcined in a muffle furnace at 800°C. The chemical properties of the catalyst were assessed as follows: 1) using X-ray diffraction (XRD) to determine the major component phase of the element; 2) using X-ray fluorescent (XRF) to determine the elemental composition of the eggshell ash; 3) using Brunauer Emmet Teller (BET) to define the structure, the surface area, pore volume and pore diameter of the eggshell ash; and 4) using SEM to show the morphology structure of the element. The XRD analysis performed on eggshell ash showed 86% CaO as a major component in the catalyst; the remaining 14% was composed of MgO, SiO2, SO3, P2O5, Na2O, Al2O3, K2O and Fe2O3, as obtained from XRF. The BET result of the catalyst prepared was characterised by large pore diameter (91.2 Å) and high surface area (30.7m2/g), allowing reactants to diffuse easily into the interior of the catalyst used